Hydrocratic generator

ABSTRACT

A hydraulic power generation system is provided for generating power using a pseudo-osmosis process which efficiently exploits the osmotic energy potential between two bodies of water having different salinity concentrations. The method and apparatus of the present invention does not require the use of a semi-permeable membrane or other specially formulated material, nor does it require heating or cooling of the fresh water or salt water solution. Moreover, the device may be used to recover energy from a wide variety of fresh water sources, including treated or untreated river run-off, treated waste-water run-off or effluent, storm-drain run-off, partly contaminated fresh water run-off, and a wide variety of other fresh water sources. The device is well suited to power production in a wide variety of geographic locations and under a wide variety of conditions. The invention has particular advantage for use in remote regions where electrical power generation by conventional means may be commercially infeasible or impractical.

This application claims benefit of Prov. No. 60/123,596 filed Mar. 10, 1999 and 60/141,349 filed Jun. 28, 1999.

BACKGROUND OF THE INVENTION

1. Field of the Invention

The present invention relates to hydraulic power generation systems and, in particular, to an apparatus and method for generating power using a novel pseudo-osmosis process which efficiently exploits the osmotic energy potential between two bodies of water having different salinity concentrations.

2. Description of the Related Art

About 20% of the world's electricity is generated using hydropower. In the United States alone this resource accounts for about 12% of the nation's supply of electricity, producing more than 90,000 megawatts of electricity annually and meeting the needs of approximately 28.3 million consumers each year. Hydropower is a clean source of natural energy. Not only is it environmentally friendly (and even beneficial in terms of flood control, etc.), but it is also extremely cost-efficient. In the Northwest, for example, electricity from hydropower plants typically costs about $10 per megawatt hour to produce. This compares to about $60, $45 and $25 per megawatt hour to produce electricity at nuclear, coal and natural gas power plants, respectively.

However, current hydroelectric power plants are configured to recover only the energy component of water that is released as a result of elevational changes. In particular, hydroelectric power is typically generated by dropping 200-300 feet-head (61-91 m-head) of fresh water from a higher elevation to a lower elevation across a rotating turbine coupled to an electrical generator. The exhaust water flow is discharged at the lower elevation as energy-depleted fresh water run-off. But, as will be explained in more detail below, this fresh water run-off is not completely depleted of energy. In fact, the amount of remaining recoverable energy in the discharged fresh water can be as great as the equivalent of 950 feet-head (290 m-head) of water or more. To understand the nature and origin of this additional recoverable energy component it is helpful to look at how fresh water is created.

Fresh water begins as water vapor that is evaporated from the oceans by solar energy. This water vapor rises into the atmosphere whereupon it cools. Cooling causes the water vapors to condense into clouds, ultimately resulting in precipitation. Some of this precipitation occurs over land masses forming fresh-water lakes, accumulated snow-fall and an extensive network of associated rivers, streams, aquifers and other forms of water run-off. Ultimately, all or virtually all of this fresh water run-off makes its way back to the oceans, thus completing the cycle. In fact, throughout the world enormous quantities of fresh water is freely washed into the ocean each year as part of the naturally occurring water cycle and/or as part of various human interventions such as hydro-power facilities, municipal waste water treatment facilities, and the like.

The overall driving force behind the water cycle is solar energy radiating from the sun over millions of square miles of exposed ocean waters each day. It is this solar energy that causes evaporation of fresh water vapors from the relatively high-saline ocean waters. The amount of radiant solar energy absorbed in this process is enormous, representing approximately 2,300 kJ/kg (0.64 kW-hr/kg) of water evaporated. This absorbed energy causes a concomitant increase in the latent energy or enthalpy of the evaporated water. The vast majority of this latent energy (approximately 99%) is dissipated as heat energy into the atmosphere upon re-condensing of the water vapors into clouds. However, a small but significant portion of this latent energy (approximately 0.13%) remains stored within the resulting fresh-water precipitation. This remaining non-dissipated stored energy represents the so-called “free energy of mixing” (or “heat of mixing”) of fresh water into sea water. Specifically, it is the additional incremental energy (beyond the energy of evaporation of pure water) that is required to separate the fresh water (or other solvent) from the salt water solution (or other solvent/solute solution).

The free energy of mixing reflects an increase in entropy of water (or other solvent) when it is transformed from its pure (fresh-water) state to its diluted (salt-water) state. It is a physical property of solvents, such as water, that they have a natural tendency to migrate from an area of relatively low solute concentration (lower entropy) to an area of relatively high solute concentration (higher entropy). Thus, an entropy gradient is created whenever two bodies of water or other solvent having differing solute concentrations are brought into contact with one another and begin to mix. This entropy gradient can be physically observed and measured in the well-known phenomena known as osmosis.

Osmosis is the flow of water through a selectively permeable membrane (i.e., permeable to water, but impermeable to dissolved solutes) from a lower concentration of solute to a higher one. It is a colligative phenomenon—that is, it is not dependent on the nature of the solute, only on the total molar concentration of all dissolved species. Pure water is defined as having an osmotic potential of zero. All water-based solutions have varying degrees of negative osmotic potential. Many references discuss osmotic potential in terms of pressure across a semi-permeable membrane since the easiest way to measure the effect is to apply pressure to the side of the membrane with higher negative osmotic potential until the net flow is canceled. “Reverse osmosis” is the phenomena that occurs when additional pressure is applied across a selectively permeable membrane to the point of reversing the natural flow-direction there-through, resulting in separation of the solvent from the solute.

But, just as it takes energy to separate an amount of fresh water from a body of salt water, such as through solar evaporation or using the well-known reverse-osmosis desalinization process, remixing the fresh water back into the ocean waters results in the release of an equal amount of stored energy (approximately 2.84 kJ/kg) of fresh water. If this source of latent stored energy could somehow be efficiently exploited, it could result in the production of enormous amounts of inexpensive electrical power from a heretofore untapped and continually renewable energy resource.

For example, if 30% of the average flow from the Columbia River could be diverted into a device that recovered this latent free energy of mixing or osmotic energy potential at 100% efficiency, it would generate 6,300 megawatts of power. To put this in perspective, the current hydroelectric facility of the Grand Coulee Dam on the Columbia River (the largest hydroelectric power plant in the United States and the third largest in the world) generates a peak output of 6,800 megawatts. If the flow from the Weber River into the Great Salt Lake could be diverted through such a device, it would generate 400 megawatts of power. Such a device would be of enormous benefit to people throughout the world, particularly those in remote regions where electrical power generation by conventional means may be difficult or impractical.

Various proposals have been made over the years for possible ways of commercially exploiting this attractive source of natural, renewable energy. For example, Jellinek (U.S. Pat. No. 3,978,344) proposed to pass fresh water through a semi-permeable membrane into a salt or brine solution. The resulting osmotic pressure differential across the membrane would then be used to eject a stream of salt water through an outlet orifice to drive a water wheel coupled to an electrical power generator to generate electrical power. Similarly, Loeb (U.S. Pat. No. 3,906,250) describes a method and apparatus for generating power utilizing pressure retarded osmosis through a semi-permeable membrane.

Each of the above approaches, like many others heretofore advocated, rely on a forward osmosis process utilizing a semi-permeable membrane to obtain useful work from the difference in osmotic potential exerted across the membrane. While such systems may have useful application on a small scale under certain limited conditions, full-scale commercial development and exploitation of such power-generation systems is hampered by the large membrane surface area required to achieve adequate flow rates and the expense and difficulty of maintaining such semi-permeable membranes. Although modem advances in synthetic materials have produced membranes that arc very efficient at rejecting brine solutes and are tough enough to withstand high pressures, such membranes are still susceptible to clogging, scaling and general degradation over time. For example, river water used as a fresh-water source would likely carry a variety of solutes and other suspended sediment or contaminants which could easily clog the membrane, requiring filtering and/or periodic cleaning. Treated effluent from a municipal waste-water treatment plant used as a fresh water source would present similar and possibly additional complications, making such approach commercially impractical.

Urry (U.S. Pat. No. 5,255,518) proposed an alternative method and apparatus for exploiting osmotic energy potential in a manner that does not utilize a semi-permeable membrane. In particular, Urry proposed the use of a specially formulated bio-elastomer. The bio-elastomer is selected such that it alternately and reversibly contracts or expands when exposed to different concentrations of a brine solution. A mechanical engine is proposed for converting the expansion and contraction motion of individual bio-elastomer elements into useful work. While such a system demonstrates the usefulness of the general approach, the proposed system utilizing bio-elastomer elements or the like is not readily suited for large-scale, low cost energy production. To produce useful energy on a commercial scale such a system would require a vast number of bio-elastic elements having very large surface area. Again, the exposed surface area would be subject to contamination and degradation over time, as with the membranes discussed above, making such a system prohibitively expensive to construct and maintain.

Assaf (U.S. Pat. No. 4,617,800) proposed another alternative apparatus for producing energy from concentrated brine in a manner that does not utilize a semi-permeable membrane or specially formulated bio-elastomer. In particular, Assaf proposed using a system of steam evaporation and re-condensation. In this approach steam is first generated by heating fresh water in an evaporator and passing the steam through a turbine to drive an electric generator. The condensed steam is then passed to a condenser wherein it is contacted with a flow of concentrated brine, generating heat from the heat of dilution of the brine. It is proposed that the evolved heat would then be transmitted though a heat-exchanger element back to the evaporator to generate steam from the fresh water. While this approach generally avoids the membrane and large surface area contamination problems discussed above, it is not ideally suited for large-scale, low cost energy production. This is because of the number and complexity of components involved and the need to heat and cool the fresh water in pressure sealed evaporator and condenser units. Such a system would be expensive to construct and operate on a commercial scale.

Thus, there remains a need for a method and apparatus for efficiently exploiting the osmotic energy potential between fresh water and sea water (and/or other solutions).

SUMMARY OF THE INVENTION

Accordingly, it is a principle object and advantage of the present invention to overcome some or all of these limitations and to provide an improved apparatus and method for generating power using a novel forward osmosis process which efficiently exploits the osmotic energy potential between two bodies of water having different salinity concentrations.

Advantageously, the method and apparatus of the present invention does not require the use of a semi-permeable membrane or other specially formulated material, nor does it require heating or cooling of the fresh water or salt water solution. Moreover, the present invention may recover energy from a wide variety of fresh water sources, including treated or untreated river run-off, treated waste-water run-off or effluent, storm-drain run-off, partly contaminated fresh water run-off, and a wide variety of other fresh water sources. Thus, the present invention is well suited to large scale power production in a wide variety of geographic locations and under a wide variety of conditions. The invention has particular advantage for use in remote regions where electrical power generation by conventional means may be commercially infeasible or impractical.

In accordance with one embodiment the present invention provides a method for generating power from the differences in osmotic potential between a source of relatively low salinity water and a source of relatively high salinity water. Relatively low salinity water is conducted through a first tube. The relatively low salinity water is then directly contacted with the relatively high salinity water in an enclosed second tube to form a mixture. The second tube is in fluid communication with the source of relatively high salinity water through one or more openings. The contacting of the two different salinity waters causes upwelling of the mixture within the second tube. This mixture is passed through a power generation unit to generate mechanical and/or electrical power.

In accordance with another embodiment the present invention provides a method for generating power from the osmotic energy potential of fresh water. A source of relatively low salinity water is conducted to a predetermined depth in a body of relatively high salinity water through a down tube having a first cross-sectional area. The relatively low salinity water is directly contacted with the relatively high salinity water from the predetermined depth in an up tube having a second cross-sectional area, forming a mixture. The mixture is allowed to upwell within the up tube upward to a depth less than the predetermined depth. The upwelling mixture is passed through a power generation unit to generate useful power.

In accordance with another embodiment the present invention provides a system for generating power from differences in osmotic potential between a source of relatively low salinity water and a source of relatively high salinity water. The system comprises an up tube located in the source of relatively high salinity water. The up tube is fluidly connected to the source of relatively high salinity water through one or more openings in the up tube at a first depth. The up tube terminates at a depth in the source of relatively high salinity water at a second depth less than the first depth. A down tube is provided having a first end connected to the source of relatively low salinity water and a second end which discharges the low salinity water from the source of relatively low salinity water into the up tube such that the relatively low salinity water and the relatively high salinity water form a mixture which upwells within the up tube. A means is provided for generating power from the rising mixture.

In accordance with another embodiment, the present invention provides a system for generating power from differences in osmotic potential between a source of relatively low salinity water and a source of relatively high salinity water. The system comprises a first tube for conducting a flow of relatively high salinity water from a first depth to a second depth, the first tube having a first cross-sectional area. A second tube is provided fluidly connected to the source of relatively low salinity water at a first end and to the first tube at a second end at or near the first depth, where the second tube has a second cross-sectional area. A third tube is provided for conducting a flow of relatively high salinity water from the second depth at or near a first end of the third tube to the first tube at the second end, where the relatively low salinity water and the high salinity water form a mixture in the first tube. The mixture is caused to flow in the first tube, increasing the recoverable energy of the relatively high salinity water in the third tube. A power generator is provided, disposed between the first and third tubes for generating power from the increase in recoverable energy.

In accordance with another embodiment, the present invention provides a method for generating power from the difference in osmotic potential between a source of relatively low salinity water and a source of relatively high salinity water. A source of relatively low salinity water is conducted through a first tube, where the first tube has a first cross-sectional area. The relatively low salinity water is directly contacted with water from the source of relatively high salinity in an enclosed second tube to form a mixture, where the second tube has a second cross-sectional area. The second tube is in fluid communication with the source of relatively high salinity water through one or more openings in a third tube. The contacting causes an increase in recoverable energy of the relatively low salinity water in the first tube. The relatively high salinity water in the third tube is conducted through a power generation unit to generate mechanical and/or electrical power.

For purposes of summarizing the invention and the advantages achieved over the prior art, certain objects and advantages of the invention have been described herein above. Of course, it is to be understood that not necessarily all such objects or advantages may be achieved in accordance with any particular embodiment of the invention. Thus, for example, those skilled in the art will recognize that the invention may be embodied or carried out in a manner that achieves or optimizes one advantage or group of advantages as taught herein without necessarily achieving other objects or advantages as may be taught or suggested herein.

All of these embodiments are intended to be within the scope of the invention herein disclosed. These and other embodiments of the present invention will become readily apparent to those skilled in the art from the following detailed description of the preferred embodiments having reference to the attached figures, the invention not being limited to any particular preferred embodiment(s) disclosed.

BRIEF DESCRIPTION OF THE DRAWINGS

Having thus summarized the general nature of the invention and its essential features and advantages, certain preferred embodiments and modifications thereof will become apparent to those skilled in the art from the detailed description herein having reference to the figures that follow, of which:

FIG. 1A is a schematic diagram representation of a conventional forward osmosis process through a semi-permeable membrane;

FIG. 1B is a schematic diagram representation of a conventional reverse osmosis process through a semi-permeable membrane;

FIG. 2 is a schematic representation of an experimental up tube upwelling apparatus for use in accordance with the present invention;

FIG. 3 is a graph of theoretical power recovery for different sized down-tubes and fresh water flow rates using the experimental upwelling device of FIG. 2;

FIG. 4 is a schematic representation of one embodiment of a hydrocratic generator having features and advantages in accordance with the present invention;

FIG. 5 is a schematic representation of an alternative embodiment of a hydrocratic generator having features and advantages in accordance with the present invention;

FIG. 6 is a schematic representation of a further alternative embodiment of a hydrocratic generator having features and advantages in accordance with the present invention;

FIG. 7A is a schematic representation of a further alternative embodiment of a hydrocratic generator having features and advantages in accordance with the present invention;

FIG. 7B is a side view of the up tube of FIG. 7A, showing the slots in the side of the up tube;

FIG. 7C is a sectional view from below of the shaft support of FIG. 7A;

FIG. 7D is a sectional view from above of the vane drum of FIG. 7A;

FIG. 8A is a schematic representation of a further alternative embodiment of a hydro-osmotic generator having features and advantages in accordance with the present invention;

FIG. 8B is a side view of the up tube of FIG. 8A showing two sets of slots in the side of the up tube;

FIG. 8C is a sectional view from below of the shaft support of FIG. 8A;

FIG. 8D is a sectional view from above of the vane drum of FIG. 8A;

FIG. 9A is a schematic view of an up tube with an open lower end with an alternative embodiment of a down tube having a plurality of holes in the sides and the outlet end, having features and advantages in accordance with the present invention;

FIG. 9B is a sectional view from below of the up tube and the outlet end of the down tube of FIG. 9A;

FIG. 10A is a schematic view of an up tube with an open lower end with an alternative embodiment of the down tube with a plurality of secondary down tubes having holes in the sides and the outlet end, having features and advantages in accordance with the present invention;

FIG. 10B is a sectional view from below of the up tube and the outlet end of the down tube of FIG. 10A showing the plurality of secondary down tubes and the holes on the outlet ends of the secondary down tubes;

FIG. 11 is a schematic view of an up tube with an open lower end with an alternative embodiment of the down tube with a plurality of secondary down tubes, having features and advantages in accordance with the present invention.;

FIG. 12 is a schematic view of a down tube with a rotating hub and spoke outlets with no up tube;

FIG. 13 is a schematic view of a down tube with a rotating hub and spoke outlets with an up tube, having features and advantages in accordance with the present invention;

FIG. 14 is a schematic view of a portion of an up tube comprising a plurality of concentric up tubes, having features and advantages in accordance with the present invention;

FIG. 15 is a schematic representation of a modified up tube having features and advantages in accordance with the present invention;

FIG. 16 is a schematic illustration of a possible large-scale commercial embodiment of a hydro-osmotic generator having features and advantages in accordance with the present invention; and

FIG. 17 is a cutaway view of the turbine and generator assembly of the hydro-osmotic generator of FIG. 12.

DESCRIPTION OF THE PREFERRED EMBODIMENTS

As discussed in the Background section above, when solvent fluids having differing osmotic potentials are contacted and mixed with each other energy is released. This released energy results from an increase in entropy of water (or other solvent) when it is transformed from its pure (fresh-water) state to its diluted (salt-water) state. Thus, an entropy gradient is created whenever two bodies of water or other solvents having differing solute concentrations are brought into contact with one another and begin to mix. This entropy gradient can be physically observed and measured in the well-known phenomena known as osmosis.

Because the term “osmosis” is associated with a membrane, the term “hydrocrasis” is used as a term for the situation when solvent fluids having differing osmotic potentials are contacted and mixed with each other in the absence of a membrane.

FIG. 1A schematically illustrates conventional forward osmosis through a semi-permeable membrane. Forward osmosis results in the flow of water 10 (or other solvent) through a selectively permeable membrane 12 from a lower concentration of solute 14 to a higher concentration of solute 14. Many references discuss osmotic potential or osmotic pressure in terms of pressure drop Π across a semi-permeable membrane since the easiest way to measure the effect is to measure the difference in height or feet (meters) of head between the high concentration side and the low concentration side of the membrane 12. Forward osmosis results in the release of work energy.

FIG. 1B illustrates the condition of reverse osmosis whereby water (or other solvent) 10 under the influence of external pressure is forced through a selectively permeable membrane 12 from a higher concentration of solute 14 to a lower concentration of solute 14, thus squeezing out or extracting the pure solvent 10 from the solute 14. Reverse osmosis is widely used in water purification and desalinization plants throughout the world. Reverse osmosis consumes work energy.

To illustrate the amount of work energy dissipated or released in the osmotic process consider a hypothetical example where a large container of salt water is supported just tinder the surface of a large open container of fresh water. Moreover, there is an osmotic membrane separating the two containers of water. Attached to the vessel of salt water and extending up out of the fresh water is a slender, tall tube with a volume of exactly one cubic meter. This slender, tall tube is open at the top, and this is the only opening to the salt water vessel. At the start of the hypothetical experiment the water level and pressure in both containers is identical and is at the bottom of the slender, tall tube. However, osmosis will cause the fresh water to flow into the container of salt water through the membrane and raise the level of salt water in the slender tall tube until the pressure exerted by the column of salt water is sufficient to just cancel or oppose the osmotic pressure across the membrane.

Now, if the top of the tube is cut just below the highest level of water therein, then salt water will begin spilling over and dropping from the top of the tube as fresh water continues to flow through the membrane into the salt water solution at an equal rate. Now, for each cubic centimeter of fresh water that flows through the membrane, an equal volume of salt water solution will be displaced from the top of the tube and drop a certain distance. Clearly, work is being done through the mechanism of osmosis, but how much work is being done? How much pressure is exerted by the column of salt water and what is the height of the column?

For small concentrations of an ideal solution, van't Hoff's formula for osmotic pressure (Π) is:

π = −CRT where; C = Molar Concentration R = Gas Constant T = Absolute temperature

For salt water there are two ions per molecule and:

wt(NaCl) = 58.5 g T = 20° C. = 293° K. R = 8.3144 J/mole° K. C = 35 ppt = 35,000 g/m³ = (35,000 ± 2/58.5 moles)/m³ = 1200 moles/m³ H = −(1200 moles/m³))(8.3144 J/mole° K.)(293° K.) = −2.9 × 10⁶ N/m² = −2.9 × 10⁶ Pa = −29 atm.

Pascal's Law says:

p=ρgh

Setting p (pressure due to the height of a column of liquid) equal to Π (the osmotic pressure) and solving for the height of the column (h) gives:

ρ = 1034 kg/m³ g = 9.8 m/s² h = (2.9 × 10⁶ N/m²)/((1034 kg/m³)(9.8 m/s²)) = 290 m

The incremental work done to displace 1 kg of water is:

W = {fraction (1/2 )}mgh = (0.5)(1 kg)(9.8 m/s²)(290 m) 1.4 kJ

Thus, the osmotic energy potential to be gained from remixing fresh water into saline ocean water is significant—about 1.4 kJ/kg of fresh water, or the equivalent of about 290 m-head of water for a conventional hydropower system. If this source of stored energy could somehow be efficiently exploited, it could result in the production of enormous amounts of inexpensive electrical power from a heretofore untapped and continually renewable energy resource.

Let us now cut the tall tube just below the maximum height of the salt water (290 meters) and attach a spigot. The salt solution would continuously flow out of the spigot. What force is generated when a kilogram of water flows through the tube and falls back to the original water level?

W = Mgh = (1 Kg)(9.8 m/s²)(290 m) = 2.8 × 10³ Joules

If the osmotic membrane had a sufficiently large surface area to allow a flow of one kilogram per second, then the system would be generating 1.4×10³ Joules per second which is the same as 1.4 Kilowatts.

If a penstock was attached to the end of the spigot and that in turn was attached to a hydroelectric generator placed at the original water level, then that generator (at 100% efficiency) would deliver 1.4 kilowatts of electrical power.

There actually would be no need for either the tall tube or the penstock. The generator would not care if the head pressure was generated by gravity or osmotic pressure. The same electricity would be generated if the opening in the salt water vessel was directly connected to the inlet of the generator.

This is, of course, not a practical system for generating electricity since it relies on an infinitely large rigid vessel and an infinitely large osmotic membrane.

While many systems have been proposed for harnessing this osmotic energy potential, few if any have been commercially successful. One problem is that most osmotic energy recovery systems rely on a conventional forward osmosis process utilizing a semi-permeable membrane. Full-scale commercial development and exploitation of such power-generation systems is hampered by the large membrane surface area required to achieve adequate flow rates and the expense and difficulty of maintaining such semi-permeable membranes. Other systems require the use of exotic bio-elastic materials and/or the use of evaporators, condensers and/or heat exchangers to extract useful work energy from osmotic energy potential.

However, in the unrelated field of ocean mariculture it is known to use the buoyancy effect of fresh water mixed with saline water to provide artificial ocean upwelling for purposes of enriching the waters in the upper photic zone of the ocean with nutrient rich waters from the lower aphotic zones. For example, U.S. Pat. No. 5,106,230, incorporated herein by reference, describes a method for the controlled generation of artificial oceanographic upwelling. The method includes introducing a relatively fresh-water input stream to a predetermined depth, where the fresh-water mixes with the nutrient-rich deep-sea water so as to form a mixture. The mixture is lifted upward by a buoyancy effect brought about by its reduced density, whereby the mixture is conducted towards the surface through an up pipe. The method results in upwelling of cold, nutrient rich water from the lower aphotic regions of the ocean to the upper photic regions where the nutrients may be beneficially used by aquatic sea life.

During recent prototype testing of a similar upwelling device it was discovered, surprisingly, that the amount of upwelling flow achieved in tenns of kinetic energy of the overall mass flow was in excess of the input energy into the system in terms of the buoyancy effect and kinetic energy resulting from the fresh water introduced into the up tube. Subsequent experiments using a modified upwelling device have confirmed that the total hydraulic energy output of such system significantly exceeds the total hydraulic energy input.

While an exact explanation for this observed phenomena is not fully appreciated at this time, it is believed that the excess energy output is somehow attributable to the release of osmotic energy potential upon remixing of the fresh water and the salt water in the up tube. This result is particularly surprising since the modified upwelling device incorporated no semi-permeable membrane or other specialized system components heretofore thought necessary to recover such osmotic energy potential. Because no membrane is present, the term hydrocratic generator is applied to the apparatus. For completeness of disclosure and understanding of the invention, the experimental design used in making this discovery is described and discussed below:

Experimental Design

An experimental upwelling apparatus similar to that illustrated in FIG. 2 was constructed using suitable corrosion resistant materials. The ocean was simulated by dissolving 1800 kilograms (2 tons) of sea salt in a 50,000 liter (15,000 gallon) swimming pool. The up tube 40 was a 15 cm (6 inch) inside diameter (i.d.) polyvinylchloride (PVC) tube 1.5 meters long. In some experiments discussed herein, the top of the up tube 40 was left open and unobstructed, as illustrated. In other experiments discussed herein, a turbine was attached to the top of the up tube 40 to convert kinetic flow energy into mechanical work energy. The down tube 20 was a 1.8 cm (½inch) i.d. (PVC) tube 1 meter long. Two 90° elbows and a short piece of pipe were attached to the end of the down tube 20 so that the fresh water was caused to exit upwards into the up tube 40 from the down tube 20. The apparatus was attached to a float 48 by nylon support cables 50, and the outlet end 44 of the up tube 40 was positioned about 15 cm below the surface of the salt water.

The down tube 20 was connected to a reservoir 25 of fresh water. The reservoir 25 was kept at a constant level by continually filling with tap water and allowing the excess to flow out the spill-way 27 so that the flow rate of fresh water through the down tube 20 was kept essentially constant. According to measurements the water in the reservoir 25 contained about 300 ppm of dissolved solids at all times, and the salt water in the swimming pool contained between 34,000 and 36,000 ppm of dissolved solids. The temperature of both the water in the reservoir 25 and the salt water was the same in any individual experiment (18-20° C.), because the salt water tank was set into the ground, and the fresh water in the reservoir came from buried pipes.

The experiment was started by filling the down tube 20 with water to eliminate air bubbles. The height of the reservoir was then adjusted to establish a pressure head that determined the rate of flow of fresh water in the down tube 20. The reservoir 25 was then filled with fresh water which was then allowed to flow from the reservoir 25 through the down tube 20 whereupon it was introduced into the lower portion of the up tube 40.

The experiment was monitored by periodically measuring the salinity at the outlet end 44 of the up tube 40 using a Myron L., DS Meter (model 512T5). The flow rate out of the outlet end 44 of the up tube 40 was calculated by measuring the salinity at the outlet end 44 of the up tube 40. In particular, FIG. 2 shows four reference points in the experimental apparatus: Point 1 is the fresh water reservoir; Point 2 is at the outlet end 44 of the up tube 40 where the salinity was measured; Point 3 is immediately above the outlet end 24 of the down tube 20; and Point 4 is inside the up tube 40 below the outlet end 24 of the down tube 20. The following salinities and densities were used in the analysis of the data.

Salinity of Salt Water=35,000 ppm

Salinity of Fresh Water=300 ppm

Density of Salt Water=1.035

Flow rates were calculated using the following analysis. Since there was a continuous tube from Point 1 to Point 3, the salinity and flow rate must be the same at Points 1 and 3. Since the only inlets to the up tube 40 are from Point 3 and Point 4, the flow at Point 2 must equal the sum of the flows at Point 3 and Point 4. The equation for the flow at Point 4 is derived from the following analysis:

If: Q1 = Flow at point i = W_(T)/p per second S_(i) = Salinity at point i = (W_(S)/W_(T)) W_(S) = Weight of Salt in a Solution W_(T) = Total Weight of Solution ρ = Density of Solution Then: S₂ = W_(S2)/W_(T2)

And since the flow past Point 2 comes from either Point 3 or Point 4:

S ₂=(W _(S3) +W _(S4))/(W _(T3) +W _(T4))

Substituting in:

W _(S) =SW _(T)

Results in:

S ₂=(S ₃ W _(T3) +S ₄ W _(T4))/(W _(T3) +W _(T4))

Substituting in:

W _(T) =Qρseconds

Results in:

S ₂=(S ₃ Q ₃ρ₃ +S ₄ Q ₄ρ₄)/(Q ₃ρ₃ +Q ₄ρ₄)

Which gives an equation that has one unknown variable (Q₄).

Q ₄ =Q ₃(ρ₃/ρ₄)(S ₂ −S ₃)/(S ₄ −S ₂)

It can be assumed, within the accuracy of this experiment, that:

S ₃=0

ρ₃=ρ₄

Which leaves:

Q ₄ =Q ₃ S ₂/(S ₄ −S ₂)

The following Examples 1-4 report the results of several experiments which were conducted using the experimental design described above and as illustrated in FIG. 2:

EXAMPLE 1

The apparatus shown in FIG. 2 was used to measure observed flow rates in the up tube 40 with different fresh water flow rates introduced into the down tube 20. Table 1 is a compilation of the results for flow rates at various points in the up tube 40 with two different flow rates of fresh water in the down tube 20. The flow rate at Point 1, the flow rate of fresh water from the reservoir, and the salinity at Point 2 at the outlet end 44 of the up tube 40 were measured parameters. The flow rate at Point 3, the outlet end 24 of the down tube 20, was the same as the flow rate at Point 1. The remaining flow rates were calculated using the equations discussed above.

TABLE I Flow Rates at Various Locations in the Up Tube Height of Reservoir Salinity at Flow (10⁻⁴ m³/sec) (meters) Point 2 (ppt) Point 1 Point 2 Point 3 Point 4 0.23 34 1.3 45.5 1.3 44.2 0.55 34 2.4 84.0 2.4 81.6

The results indicate that the flow rate of the mixed salt-water/fresh-water solution at Point 2 at the outlet end 44 of the up tube 40 far exceeded the flow rate of fresh water at Point 1 and Point 3. Introducing fresh water into the down tube 20 and allowing the salt water to flow into the up tube 40 therefore generated higher flow rates at Point 2, at the top of the up tube 40.

In order to demonstrate that this higher flow rate at Point 4 was not due to transfer of kinetic energy from the fresh water flow coming from the down tube 20, the following experiment was performed.

EXAMPLE 2 Flow Rates Through the Up Tube with Salt Water vs. Fresh Water Introduced Into the Down Tube

For this experiment, a 6″ turbine roof vent was attached to the outlet end 44 of the up tube 40. One of the vanes was painted to allow for the counting of rotations. The reservoir was filled with fresh water having a salinity of 300 ppm in one experiment and with salt water having a salinity of 36,000 ppm in a second experiment. The reservoir was placed at a height of 0.55 meters above the water level of the salt water in the pool. The fresh water was then allowed to flow through the down tube 20, and the rate at which the turbine rotated was determined. Then, salt water from the salt water pool was allowed to flow through the down tube 20, and the rate at which the turbine rotated was again determined. The results are shown in Table 2 below.

TABLE 2 Turbine Speed with Fresh Water vs. Salt Water in Down Tube Down Tube Water Flow Turbine Speed (10⁻⁴ m³/sec) (rpm) Freshwater (0.3 ppt) 2.4 5.6 Salt Water (36 ppt) 2.3 2.3

As illustrated in Table 2, above, the turbine rotated 2.4 times more rapidly when fresh water was introduced into the down tube 20 than when salt water was used. The higher turbine speed when fresh water was introduced into the down tube 20 is a direct indication that the water flow in the up tube 40 was higher when fresh water rather than salt water was introduced into the down tube 20 and that the higher observed water flow rates from the top of the up tube 40 in Example 1 were not due solely to kinetic energy transfer from the fresh water flow out of the down tube 20.

The kinetic energy transferred from the salt water in the down tube 20 to the salt water in the up tube 40 would be at least as great (if not slightly greater due to increased density of salt water) as the kinetic energy transferred from the fresh water in the down tube 20. The results shown in Table 2 indicate that some, but not all, of the upwelling of water in the up tube 40 is due to kinetic energy transfer from the water introduced into the down tube 20.

The power which is available from the kinetic energy of the water flow at various locations in the up tube 40 can be calculated as follows:

P_(k) = Power from Kinetic Energy = {fraction (1/2 )}M_(q) v² = {fraction (1/2 )}(ρQ)(16 Q²/π²d⁴) = 8 Q³ρ/π²d⁴ where: A = Cross Sectional Area = πd/4 d = Tube Diameter M_(q) = Mass Flow = Q × ρ ρ = 1 + (S_(i)/1000) v = Velocity = Q/A

Table 3 shows the calculated power attributable to kinetic energy at the three points in the up tube 40.

TABLE 3 Kinetic Energy at Various Points in the Up Tube Height of Reservoir Salinity at Kinetic Power (watts) (meters) Point 2 (ppt) Point 2 Point 3 Point 4 0.23 34 0.16 0.02 0.14 0.55 34 0.98 0.11 0.90

In the following series of experiments, the diameter of the down tube 20 and the rate of flow of the fresh water which was introduced into the down tube 20 were varied to determine the dependence of the rate of upwelling in the up tube 40 on these parameters.

EXAMPLE 3

A series of experiments were carried out using the experimental design described above and as illustrated in FIG. 2, but with down tubes 20 having different diameters. With each down tube 20, the flow rates of the fresh water in the down tube 20 were varied to determine the effect of different fresh water flow rates on available power. The salinity at the outlet end 44 of the up tube 40 was measured, and the water flow rates were calculated from the salinity as before. The water flow rates were used to calculate the available power at Point 2, the outlet end 44 of the up tube 40. The available power was then normalized by dividing the available power by the fresh water flow rate in the down tube 20. The results are shown in Table 4 below.

TABLE 4 Normalized Power Production vs. Diameter of Up Tube and Fresh Water Flow Rates Salinity at Ratio of Up Tube Power/Fresh Point 2 Flow (×0.0001 m³) Down Tube Area to Down Water Flow (ppt) Point 1 Point 4 Point 2 Area (m²) Tube Area (Watts/m³) 31.8 22 259 281 0.000254 69.7 1312 32.6 18 309 327 0.000071 249 2715 33.4 5.2 158 163 0.000018 983 1256 31.4 33 334 367 0.000254 69.7 1877 32.6 26 446 472 0.000071 249 5664 33.3 7.6 211 218 0.000018 983 2047 35.0 5 168 173 0.000010 1770 1559

In all cases, the power per unit volume of fresh water introduced into a down tube 20 of a given diameter increased as the flow rate of fresh water through the down tube 20 increased. Thus, for the down tube 20 with an area of 0.000254 m², the power/m³ of fresh water flow increased from 1312 watts/m³ with a fresh water flow rate of 22×10⁻⁴ m³ to 1877 watts/m³ with a fresh water flow rate of 33×10⁻⁴ m³. The same trend was maintained for the down tubes having areas of 0.000071 and 0.000018 m². Thus, the data illustrates that increasing the fresh water flow rate in a down tube 20 having a given area increased the normalized available power output of the device.

Second, although the power per unit volume of fresh water introduced into the down tube 20 increased with increased volume of fresh water introduced into the down tube 20 in all cases, the percent increase in the power with increase in fresh water flow rate was less for the largest down tube 20 (0.000254 m² area) than for the other down tubes 20. When the fresh water flow rate increased from 22×10⁻⁴ m³ to 33×10⁻⁴ m³, or by 50%, with the largest down tube 20, the power/fresh water flow rate increased from 1312 watts/m³ to 1877 watts/m³, or 40%. By comparison, when the fresh water flow rate for the down tube 20 with an area of 0.000018 m² was increased from 5.2 to 7.6×10⁻⁴ m³, or 46%, the power/fresh water flow rate increased from 1256 watts/m³ to 2047 watts/m³, or 62%, more than 1.5 times as much as for a comparable percent change in the fresh water flow rate with the larger down tube 20.

Similarly, when the fresh water flow rate for the down tube 20 with an area of 0.000071 m³ increased from 18 to 26×10⁻⁴ m³, or 44%, the power/fresh water flow rate increased from 2715 watts/m³ to 5664 watts/m³ or 108%, more than 2.5 times as much as for the largest down tube 20. The efficiency of power production declined with the largest diameter down tube 20.

These results are shown graphically in FIG. 3. The graphs depicted therein appear to show that there is an optimum ratio (about 250:1) of the area of the up tube 40 relative to the area of the down tube 20 that maximizes normalized power production. At ratios higher or lower than about 250 the normalized power per unit volume of fresh water declines.

Although a ratio of the area of the up tube 40 relative to the area of the down tube 20 of approximately 250 appears to be optimal, the ratio may range from approximately 5 to 50,000, more preferably from 50 to 2000.

The previous examples and discussions illustrate that a suitably constructed upwelling apparatus as illustrated in FIG. 2 has the potential of generating useful power by mixing aqueous liquids having different osmotic potentials. The simple experimental apparatus illustrated in FIG. 2 generates 0.98 watts with a fresh water flow of 2.4×10⁻⁴ cubic meters per second. This is equivalent to 4 kilowatts per cubic meter of fresh water per second, indicating an efficiency of about 0.15%. The actual efficiency and capacity of a commercial-scale power production facility will depend on a number of factors, including the size of the up tube, the ratio of the flow area of the fresh water down tube 20 to the flow area of the up tube 40, and the rate of fresh water flow. Those skilled in the art will recognize that the experimental apparatus disclosed and discussed herein-above may be modified and improved in other obvious ways to achieve even greater power production and/or efficiency of operation.

The remaining detailed discussion and corresponding figures illustrate various possible embodiments of a commercial hydrocratic generator utilizing the principles discussed above and having features and advantages in accordance with the present invention. Although the various embodiments of the apparatus depicted and described herein vary somewhat in design and operation, certain common features and advantages will become readily apparent and, thus, the descriptions thereof will not be repeated.

FIG. 4 is a simple schematic illustration of one possible embodiment of a hydrocratic generator 100 utilizing the principles discussed above and having features and advantages in accordance with the present invention. The device 100 generally comprises a down tube 20, an up tube 40, and a power plant generator 60. The particular device illustrated in FIG. 4 may be adapted for either large-scale deep water applications or for relatively small-scale or intermediate-scale power generation facilities in shallow coastal waters, as desired. For example, the depth of water illustrated in FIG. 4 may be 10 to 50 meters or more, with the up tube 40 being 1-5 meters in diameter.

In a preferred embodiment, fresh water is introduced into the down tube 20 in order to power the device. The term “fresh” water as used herein is to be interpreted in a broad sense as water having an osmotic potential relative to sea water. Thus, it may be used to describe the input stream a river discharge, a mountain run-off, a treated sewage discharge, a melting iceberg, or even runoff from a city storm drainage system.

The fresh-water input stream may be conducted though the down tube 20 by applying pressure at the inlet end 22 of the down tube 20. The pressure may be provided by a pumping station or with a hydrostatic head pressure resulting from a fluid reservoir at a higher elevation. The pressure applied at the inlet end 22 of the down tube 20 need only be high enough to overcome the hydrostatic head at the outlet end 24 of the down tube 20.

It has been found that, when fresh water is introduced into the down tube 20, sea water flows into the up tube 40, causing upwelling in the up tube 40 that can be used to generate power with the power generator 60. Some of this upwelling effect is due to the increased buoyancy of the mixed water in the up tube 20, because fresh water has a lower density than sea water. However, far more upwelling of sea water is observed than would be expected from this phenomenon alone. It is believed that the apparatus and the method is able to harness the energy available from the different osmotic potentials of fresh water and sea water. The amount of upwelling and the amount of power that is generated in the device depend in part on the particular dimensions of the up tube 40 and the down tube 20 and the flow rate of fresh water in the down tube 20.

As shown in FIG. 4, the down tube 20 has an inlet end 22 and an outlet end 24. The inlet end 22 is connected to a supply 25 of relatively fresh water. For example, this fresh water supply 25 may comprise a reservoir, pump or other source as desired or expedient. The outlet end 24 of the down tube 20 is open such that the fresh water discharges through the outlet end 24 of the down tube 20 into the up tube 40. In alternative embodiments the outlet end 24 of the down tube 20 may be connected to an intermediate mixing chamber (not shown) which then discharges into the up tube 40.

Although the down tube 20 may be any of a variety of diameters, one criterion is to choose a diameter for the down tube 20 which minimizes the resistance to fluid flow through the down tube 20. Resistance to flow through a tube decreases as the diameter of the tube increases. Choosing a large diameter for the down tube 20 therefore minimizes the resistance of the tube for a given flow rate.

Another criterion in choosing the diameter of the down tube 20 is to maximize the amount and efficiency of power generated by the power generator 60. When the diameter of the down tube 20 exceeds a certain value relative to the up tube 40, it has been discovered that the efficiency of power generation declines as the diameter of the down tube 20 is increased further. There is therefore an optimum in the ratio of the diameter of the down tube 20 relative to the diameter of the up tube 40, and therefore the ratio of the area of the down tube 20 relative to the area up tube 40, in order to maximize the efficiency of power generation. When the ratio of the area of the down tube 20 to the up tube 40 increases beyond the optimal value, the increase in efficiency of power generation with increased fresh water flow in the down tube 20 is less than with a down tube 20 having a smaller area relative to the up tube 40 area. Choosing the diameter of the down tube 20 to maximize power production therefore involves tradeoffs to choose the maximum diameter possible without losing power efficiency.

In the embodiment of the apparatus shown in FIG. 4, the outlet end 24 of the down tube 20 is located inside the up tube 40. In this embodiment, the outlet end 24 of the down tube 20 is preferably oriented so that the outlet end 24 of the down tube 20 points upward.

The up tube 40 has an lower end 42 and an outlet end 44. In the embodiment of FIG. 4 both the lower end 42 and the outlet end 44 of the up tube 40 are open. In other embodiments, the lower end 42 of the up tube 40 may contain vanes or other means of directing water flow. Some of these alternative embodiments of the up tube 40 are illustrated in other figures herein.

Although the diameters of the lower end 42 and the outlet end 44 of the embodiment of the up tube 40 shown in FIG. 4 are equal, the lower end 42 and the outlet end 44 of the up tube 40 may have different diameters in other embodiments. For example, the up tube may be positively or negatively tapered to form a nozzle or diffuser. Alternatively, the up tube 40 can have a necked-down portion to form an accelerated flow there-through.

In the embodiment of FIG. 4 the outlet end 44 of the up tube 40 is attached to a flotation system for locating the up tube 40 at a predetermined depth. Other means of locating the up tube 40 at a predetermined depth may also used in place of the flotation system, and the invention is not limited to the embodiment shown in FIG. 4. The flotation system shown in FIG. 4 comprises one or more floats 48 and one or more support cables 50. The float 48 may be formed of Styrofoam, or it may comprise a plurality of individual air bags, drums, or any other suitable material capable of producing buoyancy.

In some embodiments, the lower end 42 of the up tube 40 is attached to mooring cables 52. The mooring cables 52 extend from the lower end 42 of the up tube 40 to anchors 56 fixed on the sea floor. The mooring cables 52 and the anchors 56 retain the up tube 40 in a predetermined location on the sea floor. The lifting force of the float 48 transmitted through support cables 50 retains the up tube 40 at a desired predetermined vertical orientation.

In the embodiment shown in FIG. 4, the down tube 20 is also attached to mooring cables 52 which extend to anchors 56 on the ocean floor. The mooring cables 52 and anchors 56 hold the down tube 20 in place. The down tube 20 is arranged so that it discharges the fresh water into the up tube 40.

Just as choosing an optimal diameter for the down tube 20 involves tradeoffs, choosing the diameter of the up tube 40 also involves optimization. Increasing the diameter of the up tube 40 increases the amount of upwelling in the up tube 40 and therefore increases power production. However, increasing the diameter of the up tube 40 increases both the size and the cost of the apparatus. Further, increasing the area of the up tube 40 allows the use of a down tube 20 with a greater area without losing efficiency in generating power. The ratio of the area of the down tube 20 to the area of the up tube 40 is therefore the parameter which is to be optimized rather than the diameter of either the up tube 40 or the down tube 20 alone The optimal diameters for the up tube 40 and the down tube 20 are interdependent on one another, because the ratio of the areas of the two tubes is a more important parameter in optimizing power production than the area, and therefore the diameter, or either the up tube 40 or the down tube 20 alone.

Advantageously the down tube 20 and the up tube 40 are not subjected to excessively high pressures. In the embodiment shown in FIG. 4, the up tube 40 contains the sea water entering from the lower end 42 of the up tube 40 and the fresh water coming out of the outlet end 24 of the down tube 20. Because the up tube 40 is operated at low pressures, the up tube 40 can be constructed of relatively inexpensive and lightweight materials such as plastic, PVC, lightweight concrete, and the like.

Although the down tube 20 is subjected to higher pressures than the up tube 40, the pressures in the down tube 20 are typically small. Thus, inexpensive materials can therefore generally be used for both the up tube 40 and the down tube 20. Suitable materials for constructing the down tube 20 and the up tube 40 include, but are not limited to, polyvinyl chloride (PVC), fiberglass, polyethylene (PE), polypropylene (PP), concrete, gunite, and the like. Alternatively, other materials such as stainless steel or titanium may also be used. Because the up tube 20 and the down tube 40 are generally exposed to water of relatively high salinity, it is preferable to form the down tube 20 and the up tube 40 from materials which are resistant to corrosion from salt water. Although the materials listed above are, in general, resistant to corrosion, some alloys of stainless steel are not suitable for extended use in salt water. If stainless steel is chosen as a material of construction, it is preferable to select an alloy of stainless steel which is resistant to corrosion by salt water.

The outlet end 44 of the up tube 40 may extend to or above the surface of the sea or may be located at any depth beneath the surface of the sea. In one embodiment, the outlet end 44 of the up tube 40 is located in the photic zone so as to bring nutrient-rich deep-sea water to the photic zone to enhance growth of the organisms in the photic zone through mariculture.

The length of the up tube 40 may vary, depending on a variety of factors. The length of the up tube is preferably sufficient to allow complete mixing of the fresh water with the salt water, but not so long as to cause unnecessary drag on the water flow. The optimal length will be determined as that which allows maximum output flow rate and power production for a given range of input fresh-water flow rates. The length of the up tube 40 may also be chosen based on a desire to facilitate mariculture, the promotion of growth of organisms in the sea by transfer of nutrients from nutrient-rich depths to the nutrient-poor water at lesser depths. If mariculture is practiced, the lower end 42 of the up tube 40 is preferably located at a depth of the sea where large concentrations of nutrients are available, and the outlet end 44 of the up tube 40 is preferably located in the photic zone. In this embodiment, the up tube 40 carries nutrient-rich water from the depth of the lower end 42 of the up tube 40 to the outlet end 44 of the up tube 40 in the photic zone, where few nutrients are available, thereby enhancing growth of the organisms in the photic zone. The length of the down tube 20 is relatively unimportant, provided that it is long enough to deliver the fresh water into the up tube.

The power generator 60 generates electricity from the water flow inside the up tube 40. FIG. 4 shows one simplified form of a power generator 60 suitable for use with the present invention. The power generator 60 comprises one or more turbines or propellers 62 attached to a shaft 64. In a preferred embodiment, there are a plurality of propellers 62 attached to the shaft 64. The shaft 64 is connected to an electrical generator 66. When water upwells in the up tube 40, the upwelling water turns the propellers 62, which in turn rotate the shaft 64. The rotating shaft 64 drives the electrical generator 66, thereby generating power.

Preferably, one or more shaft supports 68 are provided to support the shaft 64 to minimize wobbling of the shaft 64 while the upwelling water turns the one or more propellers 62 attached to the shaft 64. In a preferred embodiment, a plurality of shaft supports 68 engage the shaft 64 to support the shaft 64 to minimize wobbling. In the embodiment shown in FIG. 4, three shaft supports 68 are present to support the shaft 64, a lower shaft support 68, a middle shaft support 68, and an upper shaft support 68. Further details on the shaft supports 68 are given in FIG. 7C, described later.

The propellers 62 on the shaft 64 may be inside the up tube 40, above the outlet end 44 of the up tube 40, or both inside the up tube 40 and above the outlet end 44 of the up tube 40. The propellers 62 on the shaft 64 may be located above the middle shaft support 68, below the middle shaft support 68, or both above and below the middle shaft support 68. In the embodiment of FIG. 4, the propellers 62 are located inside the up tube 40 below the middle shaft support 68. Similarly, the electrical generator 66 may be conveniently located above or below the surface of the water in which the up tube 40 is located. In the embodiment shown in FIG. 4, the electrical generator 66 is located above the surface of the water in order to minimize maintenance expense.

FIG. 5 shows an alternative embodiment of a power generator 60. In this case, the power generator 60 comprises propellers 62 attached to the shaft 64 both above and below the middle shaft support 68. The shaft 64 is attached to the electrical generator 66, which generates electrical power when the shaft 64 rotates due to the water flow in the up tube 40. Again, the electrical generator 66 of FIG. 5 is located above the surface of the water. In alternative embodiments, the electrical generator 66 may be located below the surface of the water, if desired.

FIG. 6 shows a further alternative embodiment of a power generator 60 in which one or more spiral fans 70 are mounted on the shaft 64. Shaft supports 68 may optionally be provided to minimize wobbling of the shaft 64. The one or more spiral fans 70 may be attached to the shaft 64 above the middle shaft support 68, below the middle shaft support 68, or both above and below the middle shaft support 68. One or more spiral fans 70 may be mounted on the shaft 64 on the outlet end 44 of the up tube 40. In an alternative embodiment, one or more spiral fans 70 may be mounted both inside the up tube 40 and on the outlet end 44 of the up tube 40. In the embodiment of FIG. 6, the spiral fan 70 is attached to the outlet end 44 of the up tube 40.

The spiral fan 70 comprises a plurality of spiral vanes 72. The water flow up the up tube 40 contacts the plurality of spiral vanes 72, turning the one or more spiral fans 70 mounted on the shaft 64. Turning the one or more spiral fans 70 rotates the shaft 64. The rotating shaft 64 drives the electrical generator 66, generating electrical power. Again, the electrical generator 66 may be conveniently located above or below the surface of the water, as desired.

In the embodiment of the power generator 60 shown in FIG. 6, both propellers 62 and one spiral fan 70 are mounted on the shaft 64. The propellers 62 and spiral fans 70 may be mounted on the shaft 64 in any order, above, below, or both above and below the middle shaft support 68. The propellers 62 and spiral fans 70 may also be mounted on the shaft 64 inside the up tube 40 and/or above the outlet end 44 of the up tube 40. In FIG. 6, propellers 62 are mounted on the shaft 64 inside the up tube 40 below the middle shaft support 68, and the single spiral fan 70 is mounted on the outlet end 44 of the up tube 40. The electrical generator 66 is located above the water.

FIG. 7A shows a further alternative embodiment of the up tube 40 in which the lower end 42 of the up tube 40 is closed. The down tube 20 passes through the closed lower end 42 of the up tube 40. Although FIG. 7A shows that the down tube 20 is attached to one or more mooring cables 52 which are attached to anchors 56 on the ocean floor, the down tube 20 may also be supported by the closed lower end 42 of the up tube 40. The closed lower end 42 of the up tube 40 of FIG. 7A helps to keep the down tube 20 in position without the need for mooring cables 52 and anchors 56.

The up tube 40 of the embodiment of FIG. 7A comprises a plurality of slots 76, as shown in FIG. 7B. The plurality of slots 76 are open to the surrounding sea and allow the sea water to enter the up tube 40. One or more shaft supports 68 are attached to the up tube 40. One possible embodiment of a suitable shaft support 68 is shown in FIG. 7C. The shaft support 68 comprises one or more hydrodynamic cross members 78 and a bearing 80. The cross members 78 are attached to the up tube 40 at a first end and to the bearing 80 at a second end, thereby suspending the bearing 80 inside the up tube 40. The bearing 80 can have a variety of designs such as ball bearings, compression bearings, and the like. The cross members 78 are preferably hydro-dynamically shaped so as to not slow down water flow in the up tube 40. The shaft support 68 supports the shaft 64, minimizing the wobbling of the shaft 64 when the shaft 64 rotates.

The power generator 60 of the embodiment shown in FIG. 7A comprises a vane drum 90 inside the up tube 40. The vane drum 90 comprises a plurality of rings 92 connected by a plurality of curved vanes 94. FIG. 7D shows a sectional view of the vane drum 90. Each curved vane 94 is attached by a first edge 96 to each of the plurality of rings 92. The curved vanes 94 are attached to the plurality of rings 92 in a manner so that the curved vanes 94 form a helical curve when viewed from the side, as shown in FIG. 7A. The helical curved shape of the curved vanes 94 improve the efficiency of energy transfer from the water flow through the slots 76 on the up tube 40 compared to the efficiency of curved vanes 94 which are not oriented with a helical curve. FIG. 7D shows the curved vanes 94 attached to the ring 92 from above as illustrated in FIG. 7A. FIG. 7D also shows the preferred curved surface of the curved vanes 94 as well as the helical orientation of the curved vanes 94 as viewed from above.

In one preferred embodiment, the vane drum 90 is attached to the shaft 64. When the sea water is drawn into the up tube 40 through the slots 76, the incoming water contacts the curved vanes 94, rotating the vane drum 90, which in turn rotates the shaft 64. The rotating shaft 64 turns the electrical generator 66, generating power from the upwelling water in the up tube 40.

FIG. 8A illustrates a further alternative embodiment of the power generator 60 comprising two vane drums 90, a first vane drum 90 below the middle shaft support 68 and a second vane drum 90 above the middle shaft support 68. In a preferred embodiment, both the first vane drum 90 and the second vane drum 90 are attached to the shaft 64 so that the shaft 64 rotates when the vane drums 90 rotate due to the flow of water through the slots 76 into the up tube 40. The rotating shaft 64 rotates the shaft of the electrical generator 66, generating electrical power.

In the embodiment of the up tube 40 shown in FIG. 8B, there are preferably two sets of slots 76 in the up tube 40 and two vane drums 90. In another embodiment, there are two vane drums 90 as in the embodiment shown in FIG. 8A, but the up tube 40 comprises only a single set of slots 76 in the up tube 40, as in the embodiment of the up tube 40 shown in FIG. 7B.

FIG. 9A shows an alternative embodiment of the down tube 20 in which a plurality of holes 110 are present in the side of the down tube 20. FIG. 9B shows a view of the outlet end 24 of the down tube 20 of FIG. 9A. The outlet end 24 of the down tube 20 of FIG. 9A is sealed except for a single hole 110. In alternative embodiments, a plurality of holes 110 may be provided in the outlet end 24 of the down tube 20. The fresh water flowing through the down tube 20 of FIG. 9A flows out of the plurality of holes 110 and into the up tube 40. Although the embodiment of the apparatus shown in FIG. 9A shows the alternative down tube 20 with the embodiment of the up tube 40 of FIGS. 4-6 with an open lower end 42, the down tube 20 of FIG. 9A may also be used with the embodiment of the up tube 40 such as shown in FIGS. 7A or 8A with a closed lower end 42.

FIGS. 10A and 10B show another embodiment of the down tube 20 in which the down tube 20 separates into a plurality of secondary down tubes 120 In the embodiment shown in FIG. 10A, there are a plurality of holes 110 in the secondary down tubes 120, similar to the embodiment of the down tube 20 shown in FIG. 9A. FIG. 10B shows a sectional view of the down tube 20 of the embodiment of FIG. 10A from below. In the embodiment shown in FIG. 10B the outlet end 24 of each of the five secondary down tubes 120 is closed except for a single hole 110. In the embodiment of the down tube 20 of FIGS. 10A and 10B, the fresh water that is introduced into the down tube 20 exits the holes 110 to enter the up tube 40.

In other embodiments the down tube 20 may separate into a plurality of secondary down tubes 120, as in the embodiment of the down tube 20 of FIG. 10A, but there are no holes 110 in the secondary down tubes 120, and the outlet ends 24 of the secondary down tubes 120 are open. In this embodiment of the down tube 20 (not shown), the fresh water which is introduced into the down tube 20 exits the open outlet ends 24 of the secondary down tubes 120 to enter the up tube 40.

FIG. 11 shows an alternative embodiment of the down tube 20 in which the down tube separates into a plurality of secondary down tubes 120. In the embodiment shown in FIG. 11, the down tube 20 separates into a plurality of secondary down tubes 120 outside of the up tube 40. In the embodiment shown in FIG. 11, there are no holes in the secondary down tubes 120, as in the embodiments shown in FIGS. 9A and 10A. In other embodiments there arc a plurality of holes 110 in the secondary down tubes 120.

Although the embodiment of the apparatus shown in FIG. 11 shows the alternative down tube 20 with the embodiment of the up tube 40 of FIGS. 4-6 with an open lower end 42, the alternative down tube 20 of FIG. 11 may also be used with the embodiment of the up tube 40 such as shown in FIGS. 7A or 8A with a closed lower end 42.

FIG. 12 shows another embodiment of the down tube 20 in which the down tube 20 terminates in a hub 122. The hub 122 forms a cap on the down tube 20 and rotates freely on the down tube 20. A plurality of spoke outlets 124 are fluidly connected to the hub 122. The plurality of spoke outlets 124 emerge at approximately a right angle from the hub 124 and then bend at a second angle before terminating in a spoke discharge 126. The spoke discharge 126 may have an open end or a partially closed end where the water from the down tube 20 discharges. The embodiment of the down tube 20 shown in FIG. 12 is similar to a rotating lawn sprinkler. The hub 122 is attached to the shaft 64, which is in turn connected with the electrical generator 66. In the embodiment shown in FIG. 12, there is no up tube 40.

When fresh water flows through the down tube 20 and is discharged out of the spoke outlets 124, the hub 122, shaft 64, and electrical generator 66 rotate, generating electrical power. In the embodiment shown in FIG. 12, the energy generated by the electrical generator 66 comes almost exclusively from the kinetic energy from the water emerging from the plurality of spoke discharges 126, because there is no tip tube 40 or means of generating power from hydrocratic energy generated from the mixing of fresh water from the down tube 20 with water of high salinity.

FIG. 13 shows another embodiment of the down tube 20 similar to the embodiment of FIG. 12, with a hub 122, a plurality of spoke outlets 124, and a plurality of spoke discharges 126 at the ends of the spoke outlets 124. The embodiment of FIG. 13 differs from the embodiment of FIG. 12 in that the spoke discharges 126 discharge the fresh water from the down tube 20 into an up tube 40 with an open lower end 42 and a plurality of propellers 62 attached to the shaft 64. The fresh water which exits the spoke discharges 126 into the up tube 40 causes upwelling in the up tube 40, rotating the propellers, which in turn drive the shaft 64. The shaft 64 drives a electrical generator 66 (not shown), generating electrical power.

In the embodiment of the apparatus shown in FIG. 13, the shaft 64 is rotated both by the discharge of water from the spoke discharges 126 rotating the hub 122 and by the upwelling in the up tube 40 turning the propellers 62, which in turn rotate the shaft 64. The energy generated in the embodiment of the apparatus shown in FIG. 13 is therefore a combination of kinetic energy from the rotation of the hub 122, shaft 64, and electrical generator (not shown) from the fresh water ejected from the spoke discharges 126 and from hydrocratic energy generated from the upwelling in the up tube 40 from the mixing of fresh water from the spoke discharges 126 mixing with the water of high salinity entering the up tube 40 from the lower end 42.

FIG. 14 illustrates another embodiment of the up tube 40 in which there are a plurality of nested up tubes 40 having increasing diameters. The lower end 42 of each of the plurality of nested up tubes 40 is open. Fresh water is introduced into the down tube 20 causing upwelling in the plurality of up tubes 40 when the water of high salinity enters the open lower ends 42 of the nested up tubes 40.

Any of the embodiments of power generators 60 can be combined with the embodiment of the nested up tubes 40 of FIG. 14. For example, in one embodiment, the propellers 62 of FIGS. 4 and 5 may be used as a power generator 60 in combination with the nested up tubes 40 of FIG. 14. In another embodiment, the power generator 60 may comprise one or more spiral fans 70, as shown in FIG. 6.

FIG. 15 shows another embodiment of the up tube 40 and power generator 60. In the embodiment of FIG. 15, a plurality of turbines 130 are mounted on a shaft 64 inter-spaced between a plurality of stators 132. The stators 132 direct the water flow into the turbine blades of the turbines 130 to increase the efficiency thereof. The shaft 64 is connected to an electrical generator 66 (not shown). When water upwells in the up tube 40, the upwelling water turns the turbines 130, which in turn rotate the shaft 64 and the electrical generator 66, generating power.

In the embodiment shown in FIG. 15, the portion of the up tube 40 surrounding the turbines 130 and stators 132 comprises a nozzle 134 and an expander 136. The nozzle 134 reduces the diameter of the up tube 40 in the portion of the up tube 40 around the turbines 130 and stators 132 from the diameter of the remainder of the up tube 40. By reducing the diameter of the up tube 40 with the nozzle 134 in the portion of the up tube 40 surrounding the turbines 130, the upwelling water is forced into a smaller area and is accelerated to a higher velocity water flow that can be harnessed more efficiently by the turbines 130. Nozzles 134 and stators 132 can also be used with other embodiments of the power generator 60 illustrated herein.

FIG. 16 is a schematic illustration of a possible large-scale commercial embodiment of a hydrocratic generator having features and advantages of the present invention. While a particular scale is not illustrated, those skilled in the art will recognize that the device 200 is advantageously suited for large-scale deep-water use 100-500 meters or more beneath sea level. The up tube 240 extends upward and terminates at any convenient point beneath sea level. The diameter of the up tube may be 3-20 meters or more, depending upon the desired capacity of the hydrocratic generator 200. This particular design is preferably adapted to minimize environmental impact and, therefore, does not result in upwelling of nutrient rich water from the ocean depths.

Sea water is admitted into the device from an elevated inlet tube 215 through a filter screen or grate 245. The filter removes sea life and/or other unwanted objects or debris that could otherwise adversely impact the operation of generator 200 or result in injury to local sea life population. If desired, the inlet tube 215 may be insulated in order to minimize heat loss of the siphoned-off surface waters to colder water at or near full ocean depth. Advantageously, this ensures that the temperature and, therefore, the density of the sea water drawn into the generator 200 is not too cold and dense to prevent or inhibit upwelling in the up tube 240.

The sea water is passed through a hydraulic turbine power plant 260 of the type used to generate hydraulic power at a typical hydro-electric facility. The turbine and generator assembly is illustrated in more detail in the cutaway view of FIG. 16. Water enters the turbine 261 through a series of louvers 262, called wicket gates, which are arranged in a ring around the turbine inlet. The amount of water entering the turbine 261 can be regulated by opening or closing the wicket gates 262 as required. This allows the operators to keep the turbine turning at a constant speed even under widely varying electrical loads and/or hydraulic flow rates. Maintaining precise speed is desirable since it is the rate of rotation which determines the frequency of the electricity produced.

As illustrated in FIG. 16, the turbine is coupled to an electric generator 266 by a long shaft 264. The generator 266 comprises a large, spinning “rotor” 267 and a stationary “stator” 268. The outer ring of the rotor 267 is made up of a series of copper wound iron cells or “poles” each of which acts as an electromagnet. The stator 268 is similarly comprised of a series of vertically oriented copper coils disposed in the slots of an iron core. As the rotor 267 spins, its magnetic field induces a current in the stator's windings thereby generating alternating current (AC) electricity.

Referring again to FIG. 16, the sea water is discharged from the turbine into the up tube 240. Fresh water is introduced into the base of the up tube 240 by down tube 220. The mixing of fresh water into saline sea water releases the hydrocratic or osmotic energy potential of the fresh water in accordance with the principles discussed above, resulting in a concomitant pressure drop (up to 190 meters of head) across the hydraulic turbine 260. This pressure drop in conjunction with the induced water flow upwelling through the up tube 240 allows for generation of significant hydro-power for commercial power production applications without adversely affecting surrounding marine culture.

Other Applications/Embodiments

In the preferred embodiments discussed above, the up tube 40 is located in a body of water of high salinity and high negative osmotic potential such as an ocean or a sea. The water of high salinity and high negative osmotic potential enters the up tube 40 in a ratio of greater than 8:1 salt water to fresh water, more preferably 30:1 salt water to fresh water, and most preferably about 34:1 or higher. The mixing of the fresh water of low negative osmotic potential with the sea water of high negative osmotic potential in the up tube 40 causes upwelling and draws sea water into the up tube 40 through the openings. The upwelling water in the up tube 40 rotates propellers 62, spiral fans 70 or turbines 130, 261, which are attached to a drive shaft 64, 264. The rotating shaft 64, 264 turns the electrical generator 66, 266 generating electrical power from the difference in osmotic potential between the fresh water introduced into the down tube 20 and the water of high salinity which enters the up tube 40 through the openings in the up tube 40.

Because the method depends on having solutions of different osmotic potentials exiting the down tube 20 and entering the up tube 40, it is preferable that the source of fresh water exiting the down tube 20 and the source of the water of high salinity entering the up tube 40 continue to have different osmotic potentials over time so that power generation continues over a long period of time. For example, if the body of water of high salinity surrounding the up tube 40 is small, the fresh water exiting the down tube 20 can dilute the water of high salinity after exiting the up tube 40, reducing the difference in osmotic potential between the fresh water and the water of high salinity. Reducing the difference in osmotic potential between the fresh water exiting the down tube 20 and the water of high salinity entering the up tube 40 reduces the amount of energy available. It is therefore generally advantageous that the body of water of high salinity have a large volume. Locating the up tube 40 in a large body of water having high salinity such as the ocean or the Great Salt Lake is therefore a preferred embodiment.

Alternatively, the invention can be operated between bodies of salt water having different salinity or between waters at different depths of the same body of water. For example, the salinity and temperature of sea water is known to vary with depth and location. In the Hawaiian islands, at a depth of 1000 meters, the ambient water temperature is approximately 35° F., with a salinity of approximately 34.6 ppt. The surface temperature is approximately 80° F. with a salinity of approximately 35.5 ppt. Thus, an osmotic energy potential (albeit small) exists between the surface waters and the waters at 100 meters depth.

While the present invention is disclosed in the context of generating power by directly contacting and mixing fresh water with sea water in an apparatus located in the ocean, it is to be understood that the apparatus and method are not limited to this embodiment. The techniques and concepts taught herein are also applicable to a variety of other situations where aqueous solutions having differing osmotic potentials are available. For example, in one embodiment, the apparatus and method may be applied to a concentrated brine from a desalinization plant being mixed with the less-concentrated brine in sea water. In another embodiment, a treated sewage effluent, a fresh water stream, can be mixed with sea water. If desired, an osmotic membrane or osmotic water exchange plenum may be provided at the outlet end of the down tube and/or at the outlet (top) of the up tube in order to increase the efficiency of energy production. The apparatus and method may thus be applied to a wide range of applications in which two solutions of differing osmotic potential are available.

The various embodiments of the invention disclosed and described herein are exemplary only. As such, these example embodiments are not intended to be exhaustive of all possible ways of carrying out the invention or even the most economical or cost-efficient ways of carrying out the invention on a commercial scale. Many of the example embodiments disclosed and discussed herein are based on experimental testing of small-scale models embodying certain features of the invention. These models and the test results reported herein may or may not be directly relevant to a full-scale power production facility utilizing the invention. However, those skilled in the art will readily recognize from the examples disclosed and discussed herein the utility of the invention in terms of its broader scope, and how it may be beneficially utilized in a commercial power production facility to efficiently harness the osmotic energy potential between fresh water run-off and sea water (or other convenient bodies of water/solvent having different solute concentrations).

Thus, although this invention has been disclosed in the context of certain preferred embodiments and examples, it will be understood by those skilled in the art that the present invention extends beyond the specifically disclosed embodiments to other alternative embodiments and/or uses of the invention and obvious modifications and equivalents thereof. Accordingly, it is intended that the scope of the present invention herein disclosed should not be limited by the particular disclosed embodiments described above, but should be determined only by a fair reading of the claims that follow. 

What is claimed is:
 1. A method for generating power from the difference in osmotic potential between a source of relatively low salinity water and a source of relatively high salinity water, said method comprising: conducting the source of relatively low salinity water through a first tube; directly contacting relatively low salinity water with water from the source of relatively high salinity in an enclosed second tube to form a mixture, wherein said second tube is in fluid communication with the source of relatively high salinity water through one or more openings, said contacting causing an increase in recoverable energy of said mixture in said second tube; and conducting said mixture through a power generation unit to generate mechanical and/or electrical power.
 2. The method of claim 1, wherein said power generation unit comprises: a plurality of propellers on a shaft, said propellers being located inside said second tube; and an electrical generator coupled to said shaft for generating electrical power.
 3. The method of claim 1, wherein said power generation unit comprises: a vane drum comprising a plurality of vanes, wherein said plurality of vanes rotate a shaft when contacted with said mixture; and an electrical generator connected to said shaft.
 4. The method of claim 3, wherein said vanes are connected with said shaft through a plurality of rings.
 5. The method of claim 3, wherein said power generation unit comprises: a spiral fan on a shaft, wherein said spiral fan is mounted inside or on top of said second tube; and an electrical generator connected to said shaft.
 6. A method of generating power from the osmotic energy potential of fresh water comprising: conducting a source of relatively low salinity water to a predetermined depth in a body of relatively high salinity water through a down tube, said down tube having a first cross-sectional area; directly contacting the relatively low salinity water with the relatively high salinity water from the predetermined depth in an up tube to form a mixture, said up tube having a second cross-sectional area; allowing the mixture to upwell within the up tube upward to a depth less than the predetermined depth; and passing the mixture through a power generation unit to generate useful power.
 7. The method of claim 6, wherein the source of relatively high salinity water is an ocean.
 8. The method of claim 6, wherein the source of relatively low salinity water is fresh water run off from a land source.
 9. The method of claim 6, wherein said first cross-sectional area is 5 to 50,000 times smaller than said second cross-sectional area.
 10. The method of claim 6, wherein said first cross-sectional area is 50 to 2000 times smaller than said second cross-sectional area.
 11. The method of claim 6, wherein said first cross-sectional area is approximately 250 times smaller than said second cross-sectional area.
 12. The method of claim 6, wherein said mixture comprises said high salinity water and said relatively low salinity water in a ratio of at least 8:1.
 13. The method of claim 6, wherein said mixture comprises said high salinity water and said relatively low salinity water in a ratio of at least 30:1.
 14. The method of claim 6, wherein said mixture comprises said high salinity water and said relatively low salinity water in a ratio of approximately 34:1.
 15. A system for generating power from differences in osmotic potential between a source of relatively low salinity water and a source of relatively high salinity water, said system comprising: an up tube located in said source of relatively high salinity water, wherein said up tube is fluidly connected to said source of relatively high salinity water through one or more openings in said up tube at a first depth and wherein said up tube terminates at a depth in said source of relatively high salinity water at a second depth, said second depth being less than said first depth; a down tube having a first end connected to the source of relatively low salinity water and a second end which discharges the low salinity water from said source of relatively low salinity water into said up tube, wherein said relatively low salinity water and said relatively high salinity water form a mixture, wherein said mixture rises in said up tube; and means for generating power from the rising mixture.
 16. The system of claim 15, wherein the source of relatively high salinity water is an ocean.
 17. The system of claim 15, wherein the source of relatively low salinity water is fresh water run off from a land source.
 18. The system of claim 15, wherein said first cross-sectional area is 5 to 50,000 times smaller than said second cross-sectional area.
 19. The system of claim 15, wherein the cross-sectional area of said down tube is 50 to 2000 times smaller than the cross-sectional area of said up tube.
 20. The system of claim 15, wherein said power generation means comprises a plurality of propellers on a shaft, said propellers being located inside said up tube and an electrical generator coupled to said shaft for generating electrical power.
 21. The system of claim 15, wherein said power generation means comprises a vane drum comprising a plurality of vanes, wherein said plurality of vanes rotate a shaft when contacted with said upwelling mixture and an electrical generator connected to said shaft.
 22. The system of claim 21, wherein said vanes are connected with said shaft through a plurality of rings.
 23. The system of claim 15, wherein said power generation means comprises a spiral fan on a shaft, wherein said spiral fan is mounted inside or on top of said up tube and an electrical generator connected to said shaft.
 24. A system for generating power from differences in osmotic potential between a source of relatively low salinity water and a source of relatively high salinity water, said system comprising: a first tube for conducting a flow of relatively high salinity water from a first depth to a second depth, said first tube having a first cross-sectional area; a second tube fluidly connected to the source of relatively low salinity water at a first end and to said first tube at a second end at or near said first depth, said second tube having a second cross-sectional area; a third tube for conducting a flow of relatively high salinity water from said second depth at or near a first end of said third tube to said first tube at said second end, wherein said relatively low salinity water and said high salinity water form a mixture in said first tube, wherein said mixture is caused to flow in said first tube, increasing the recoverable energy of said relatively high salinity water in said third tube; and a power generator disposed between said first and third tubes for generating power from said increase in recoverable energy.
 25. The system of claim 24, wherein the source of relatively high salinity water is an ocean.
 26. The system of claim 24, wherein the source of relatively low salinity water is fresh water run off from a land source.
 27. The system of claim 24, wherein said second cross-sectional area is 5 to 50,000 times smaller than said first cross-sectional area.
 28. The system of claim 24, wherein the cross-sectional area of said second tube is 50 to 2000 times smaller than the cross-sectional area of said first tube.
 29. A method for generating power from the difference in osmotic potential between a source of relatively low salinity water and a source of relatively high salinity water, said method comprising: conducting the source of relatively low salinity water through a first tube, said first tube having a first cross-sectional area; directly contacting relatively low salinity water with water from the source of relatively high salinity in an enclosed second tube to form a mixture, said second tube having a second cross-sectional area, wherein said second tube is in fluid communication with the source of relatively high salinity water through one or more openings in a third tube, said contacting causing an increase in recoverable energy of said relatively high salinity water in said third tube; and conducting said relatively high salinity water in said third tube through a power generation unit to generate mechanical and/or electrical power.
 30. The method of claim 29, wherein the source of relatively high salinity water is an ocean.
 31. The method of claim 29, wherein the source of relatively low salinity water is fresh water nin off from a land source.
 32. The method of claim 29, wherein said first cross-sectional area is 5 to 50,000 times smaller than said second cross-sectional area.
 33. The method of claim 29, wherein said first cross-sectional area is 50 to 2000 times smaller than said second cross-sectional area.
 34. The method of claim 29, wherein said first cross-sectional area is approximately 250 times smaller than said second cross-sectional area.
 35. The method of claim 29, wherein said mixture comprises said high salinity water and said relatively low salinity water in a ratio of at least 8:1.
 36. The method of claim 29, wherein said mixture comprises said high salinity water and said relatively low salinity water in a ratio of at least 30:1.
 37. The method of claim 29, wherein said mixture comprises said high salinity water and said relatively low salinity water in a ratio of approximately 34:1. 